Abstract:
A method for the continuous manufacture of bisphenol A comprising i) feeding one or more feed streams comprising phenol and acetone to a reactor and reacting said acetone and phenol in the presence of an ion-exchange resin catalyst thereby forming a product stream comprising bisphenol A, phenol, acetone, water and by-products, ii) crystallising bisphenol A and/or bisphenol A/phenol adduct crystals from said product stream in one or more crystallisation units thereby forming a slurry consisting of said crystals and a mother liquor, iii) separating the mother liquor from the crystals in one or more solid-liquid separation units, iv) heating the mother liquor in a heat recovery unit and feeding the heated mother liquor to a distillation column, v) separating the mother liquor in the distillation column thereby forming a bottom stream comprising phenol and a top stream comprising water, vi) cooling the bottom stream in said heat recovery unit.
Abstract:
The present invention provides an annular centrifugal contactor, having a housing to receive a plurality of liquids; a rotor inside the housing; an annular mixing zone, with a plurality of fluid retention reservoirs; and an adjustable stem that can be raised to restrict the flow of a liquid into the rotor or lowered to increase the flow of liquid into the rotor. The invention also provides a method for transferring moieties from a first liquid to a second liquid, the method having the steps of combining the fluids in a housing whose interior has helically shaped first channels; subjecting the fluids to a spinning rotor to produce a mixture, whereby the channels simultaneously conduct the mixture downwardly and upwardly; and passing the mixture through the rotor to contact second channels, whereby the channels pump the second liquid through a first aperture while the first fluid exits a second aperture.
Abstract:
The present invention provides an annular centrifugal contactor, having a housing adapted to receive a plurality of flowing liquids; a rotor on the interior of the housing; an annular mixing zone, wherein the annular mixing zone has a plurality of fluid retention reservoirs with ingress apertures near the bottom of the annular mixing zone and egress apertures located above the ingress apertures of the annular mixing zone; and an adjustable vane plate stem, wherein the stem can be raised to restrict the flow of a liquid into the rotor or lowered to increase the flow of the liquid into the rotor.
Abstract:
The present invention provides an annular centrifugal contactor, having a housing adapted to receive a plurality of flowing liquids; a rotor on the interior of the housing; an annular mixing zone, wherein the annular mixing zone has a plurality of fluid retention reservoirs with ingress apertures near the bottom of the annular mixing zone and egress apertures located above the ingress apertures of the annular mixing zone; and an adjustable vane plate stem, wherein the stem can be raised to restrict the flow of a liquid into the rotor or lowered to increase the flow of the liquid into the rotor.
Abstract:
A membrane-integrated hydration reactor that is operable to produce an associated alcohol product from an olefin using water includes a solid acid olefin hydration catalyst in a production zone and a hydrophilic membrane operable to selectively permit pervaporation of water one-way and not permit pervaporation of the associated alcohol or permeation of the olefin at olefin hydration process conditions in a separations zone. The production zone is operable to form a production zone product mixture made of the associated alcohol and any unreacted water. The associated separations zone is operable to form and produce both the associated alcohol product and a pervaporated water product from the production zone product mixture. A method of olefin hydration for forming an associated alcohol product from an olefin using water uses the membrane-integrated hydration reactor at olefin hydration process conditions.
Abstract:
The present disclosure relates to an apparatus and process for forming medical devices from an injectable composition. The apparatus includes a supply assembly configured to maintain and selective dispense a first precursor and a second precursor, a mixing assembly configured to mix the first and second precursors, and at least one catalyzing element including a transition metal ion to aid in the polymerization of the first and second precursors. The process includes dispensing a volume of the first precursor and a volume of the second precursor into a mixing assembly and mixing the first and second precursors. The first and second precursors each possess a core and at least one functional group known to have click reactivity with each other. The mixed precursors are contacted with a transition metal catalyst to produce a flowable composition for use as a medical device.
Abstract:
A carbonylation process for producing acetic acid including: (a) carbonylating methanol or its reactive derivatives in the presence of a Group VIII metal catalyst and methyl iodide promoter to produce a liquid reaction mixture including acetic acid, water, methyl acetate and methyl iodide; (b) feeding the liquid reaction mixture at a feed temperature to a flash vessel which is maintained at a reduced pressure; (c) heating the flash vessel while concurrently flashing the reaction mixture to produce a crude product vapor stream, wherein the reaction mixture is selected and the flow rate of the reaction mixture fed to the flash vessel as well as the amount of heat supplied to the flash vessel is controlled such that the temperature of the crude product vapor stream is maintained at a temperature less than 90° F. cooler than the feed temperature of the liquid reaction mixture to the flasher and the concentration of acetic acid in the crude product vapor stream is greater than 70% by weight of the crude product vapor stream.
Abstract:
A catalytic static mixing reactor has a conduit casing defined about an axis of a fluid flow. A catalyst is deposited on a mixing element. The mixing element is adapted to be inserted in the conduit. The element provides an exceptionally high surface area and is formed to obstacle the primary flow inducing a first order mixing phenomenon. The element is formed with at least one irregular surface or edge capable of inducing a second order mixing phenomenon. The irregular surface is adapted as a catalytic supporting surface. The supporting surface supports the deposition of the catalyst thereon so that a third order chemical reaction phenomenon is coupled with that of said first and second order mixing phenomenon at the catalytic surface so that a reactant to be converted in the fluid flow is converted to at least one predetermined product during said first and second order mixing phenomenon.
Abstract:
Surface-active solid-phase catalyst activity may be substantially improved by creating deliberate repetitive surface-to-surface contact between portions of the active surfaces of catalyst objects. While they are immersed in reactant material such contact between portions of the active surfaces of catalyst objects can substantially activate the surfaces of many heterogeneous catalysts. Examples are given of such action employing a multitude of predetermined shapes, supported catalyst structures, etc. agitated or otherwise brought into contact to produce numerous surface collisions. One embodiment employs a gear pump mechanism with catalytically active-surfaced gear teeth to create the repetitive transient contacting action during pumping of a flow of reactant. The invention is applicable to many other forms for creating transient catalytic surface contacting action. Optionally catalytic output of such systems may be significantly further improved by employing radiant energy or vibration.
Abstract:
Chemical process accelerator systems comprising viscid fluid Taylor Vortex Flows (98, 50a) with high-shear-rate laminar Circular Couette Flows (58) in contact with catalysts (92, 92′, 30, 32, 32f, 32g, 36, 40, 44, 45, 46, 47, 48), catalytic compositions and structures in chemical reactors and electrochemical cells (e.g. fuel cells, fuel reformers) are disclosed.